Concept
Total capex is the full one-time capital to deliver a working plant — the equipment build rolled all the way up: installed process units (ISBL), plus off-site infrastructure (OSBL), plus indirects (engineering, fees, contingency), plus working capital. It’s the loaded figure that gets annualized and divided into levelized cost — not the bare equipment or ISBL cost.
What “total” adds to the equipment build. Capex as the equipment build stops at installed ISBL. The standard factored roll-up from there:
= total capex (total project capital).
Each layer multiplies the one beneath. OSBL factors ISBL, indirects factor direct field cost, contingency factors that — a stack of multipliers (see battery limits), so an ISBL-base error scales through every layer to the total. The Lang factor is the one-step shortcut that collapses the whole stack into a single multiple of purchased-equipment cost.
Contingency tracks the estimate’s maturity — larger when less resolved, a feature of the accuracy class, not a worse project. Dropping it to report a lower number reports a best case the accuracy class says is unlikely.
What it feeds. This is the figure the capital recovery factor annualizes, which — spread over output — becomes the capital share of levelized cost. When a TEA quotes “the capex,” this is the defensible figure.
Rolling the green ammonia plant up from ISBL. Take installed ISBL ≈ $500M as a round, illustrative anchor (order-of-magnitude for a ~1,000 t/day plant). + OSBL at ~40% of ISBL (the battery-limits anchor) → direct field cost ~$700M; + ~30% indirects and contingency → total fixed capital ~$910M; + $90M working capital → total capex **$1.0bn**. That ~$1.0bn — not the $500M ISBL — is carried into the capital recovery factor and levelized cost.
Edge case: reporting the $500M ISBL as the project’s “capex” would halve the apparent capital and, once annualized, halve the capital share of the per-tonne cost — the classic understatement from quoting the inside-the-fence figure as the whole plant.